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Process Equipment and Plant Design

Process Equipment and Plant Design
The safe height (h) to diameter (d) ratio (i.e., h/d) for liquid/petro fuel storage tank of capacity more than 45 kilolitres is less than

2
1
3
3.5

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Process Equipment and Plant Design
Stage efficiency for packed tower varies with the

Type & size of packing
Fluid rates and fluid properties
All of these
Operating pressure and column diameter

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Process Equipment and Plant Design
The optimum size ratio for two mixed reactors in series depends on the kinetics of the reaction and the conversion level. For reaction orders more than one, the

Equal sized reactors are the best
Smaller reactor should come first
None of these
Larger reactor should come first

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Process Equipment and Plant Design
Baffles may be eliminated for

High viscosity liquids (> 600 poise)
None of these
Large diameter tanks
Low viscosity liquids (< 200 poise)

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Process Equipment and Plant Design
Power required for agitation depends upon the

Height & properties of the liquid
Agitator type & speed of agitation
All of these
Size of agitator & the tank

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Process Equipment and Plant Design
Which of the following packing materials provides for maximum mass transfer?

All of these
Lessig rings
Raschig rings
Cross-partition rings

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